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Hybrid Process (hybrid + process)

Distribution by Scientific Domains

Chemistry	53%
Engineering	38%

Selected Abstracts

Deposition of TiN,WS2 Nanocomposite Coatings by a Hybrid Process: Reactive Sputtering and Clusters Gun

PLASMA PROCESSES AND POLYMERS, Issue S1 2009
D. Bharathi Mohan
Abstract A dc magnetron reactive sputtering equipment connected with a homemade clusters gun was used to deposit a series of TiN,WS2 nanocomposite coatings with different magnetron power values and different argon pressures in the clusters gun. The original idea was to achieve from the TiN matrix, originated from the normal running of the magnetron system, the high wear resistance property, whereas the pre-formed IF,WS2 nanospheres introduced by the clusters gun would provide the low friction coefficient. A small peak detected at low diffraction angles by X-ray diffraction in two of the produced samples gave the first evidence of the WS2 nanospheres incorporation in the TiN matrix. Then, scanning electron microscopy was used for observing very small grain features which were identified as the WS2 nanospheres by energy dispersive analysis of X-rays, demonstrating the feasibility of this hybrid technique for the deposition of nanocomposite coatings. [source]

L -Lysine Monohydrochloride Syrup Concentration using a Membrane Hybrid Process of Ultrafiltration and Vacuum Membrane Distillation

CHEMICAL ENGINEERING & TECHNOLOGY (CET), Issue 11 2008
O. Bakhtiari
Abstract The development of energy saving membrane separation processes is finding a unique position in process industries. One of the important areas where they are employed is the biotechnology industry. This industry has its own specifications and requirements, e.g., levels of diluteness, thermal, chemical and shear fragility. Membrane separation processes have the characteristics necessary to match these specifications and needs. In this research, the determination of the experimental concentration of L -Lysine monohydrochloride (L -lysine-HCl) syrup was investigated using ultrafiltration (UF) and vacuum membrane distillation (VMD) hybrid membrane processes. Four parameters that are known to have significant influence on the UF process were examined, i.e., pressure difference across the membrane, feed concentration of L -lysine-HCl, feed velocity on the membrane surface, and pH. For the VMD unit, pressure difference and pH were replaced with feed temperature and vacuum pressure on the permeate side of membrane. Each process was carried out separately and the results were used to design a bench-scale process. In order to save time and money, the Taguchi method of experimental design was employed. The effects of feed concentration, pressure difference across the membrane, feed velocity on the membrane surface, and pH on the target variable, i.e., the membrane flux, in the UF process were 39.93, 38.65, 9.36, and 9.59,%, respectively. For the VMD process, these values were 64.79, 22.16, 6.21, and 2.14,% for feed temperature, feed concentration, vacuum pressure on the permeate side, and feed velocity on the membrane surface, respectively. [source]

Auslegung und Optimierung von hybriden Trennverfahren,

CHEMIE-INGENIEUR-TECHNIK (CIT), Issue 3 2004
M. Franke Dipl.-Ing.
Abstract Unter hybriden Trennverfahren versteht man die Verschaltung von mindestens zwei verschiedenen, apparativ getrennten Grundoperationen, die zur Trennaufgabe beitragen. Hybride Trennverfahren werden bei schwierigen Trennungen, wie bei engsiedenden oder azeotropen Gemischen, eingesetzt, wenn eine einzelne Grundoperation, z.,B. Rektifikation, Extraktion, Kristallisation, Membranverfahren oder Chromatographie, gar nicht oder nur mit sehr großem Aufwand zum Ziel führt. Aufgrund der Struktur des Hybridprozesses, die das Vorhandensein mindestens zwei verschiedener Grundoperationen und eine entsprechende Anzahl von Rückführungen impliziert, ist die Auslegung komplex, sie wird deshalb z.,Z. systematisch in der Forschung untersucht. In dieser Arbeit werden die Anforderungen an eine Auslegungsmethodik für hybride Trennverfahren dargestellt. Es wird eine Methodik vorgestellt, die auf einer detaillierten Modellierung der Grundoperationen und einer simultanen Mehrvariablen-Optimierung beruht. Die Anwendbarkeit dieser Methodik wird anhand einer Isomerentrennung gezeigt. Design and Optimization of Hybrid Separation Processes Hybrid separation processes are defined as the combination of at least two different unit operations in different apparatus which contribute to the separation task. Hybrid processes are used for difficult separations, e.g., close-boiling mixtures and azeotropes, if a single unit operation, e.g., distillation, membranes, extraction, crystallization or chromatography, is not efficient or even not feasible. Because of the structure of a hybrid process which implies two or more unit operations and recycle streams, the design is not straightforward and therefore subject of today's research. In this work general criteria for such a consistent design method are described and a design approach for hybrid separation processes is presented. It bases on rigorous modeling of the unit operations and simultaneous multivariable optimization. The approach feasibility is demonstrated by the separation of an isomer mixture. [source]

Hydrophobic pervaporation for environmental applications: Process optimization and integration

ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, Issue 4 2002
Frank Lipnizki
The focus of this paper is on the design of pervaporation units for wastewater treatment taking into account technical, economic, and environmental aspects. Two different sized industrial wastewater streams of water-chloroform, and of water-methyl-isobutylketone (MIBK) are considered. Based on a wastewater stream of 1,500 kg/d, a semi-batch process combining pervaporation with a decanter recycle loop is developed. Using this process, it is possible to recover over 99% of the organic components at concentrations of more than 98 wt. %. The treatment costs are between 0.11 to 0.16 $/kg wastewater. For the treatment of a wastewater stream of 1,000 kg/h, pervaporation combined with a decanter and recycling loop, as well as integrated in a hybrid process with adsorption, is considered. For MIBK, pervaporation with a decanter is the most attractive option taking economic and environmental aspects into account, while, for chloroform, the hybrid process is the better option. Treatment costs in all cases are about 0.03 $/kg wastewater. The recovery rate of the organic compounds is over 99% at concentrations over 98 wt. %. The authors concluded that pervaporation as a stand-alone unit, or integrated into hybrid processes, offers significant advantages over conventional alternatives. [source]

Plant-wide control of a hybrid process

INTERNATIONAL JOURNAL OF ADAPTIVE CONTROL AND SIGNAL PROCESSING, Issue 2 2008
C. de Prada
Abstract This paper deals with the model predictive control (MPC) of an industrial hybrid process where continuous and batch units operate jointly: the crystallization section of a sugar factory. The paper describes a plant-wide predictive controller that takes into account, both, continuous objectives and manipulated variables, as well as those related to the discrete operation and logic of the batch units. The MPC is formulated with time events, so that a more efficient NLP optimization technique, instead of MINLP, could be applied. Adaptation is provided by model updating and error estimation. Results of the controller operation in an industrial simulator are provided. Copyright © 2007 John Wiley & Sons, Ltd. [source]

Liquid phase mineralization of gel-type anion exchange resin by a hybrid process of Fenton dissolution followed by sonication and wet air oxidation

ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, Issue 1 2009
T. L. Gunale
Abstract A hybrid process of Fenton dissolution followed by sonication and wet air oxidation (WAO), has been demonstrated to mineralize strongly basic anion exchange resin (gel type). The solid anion exchange resin beads could be dissolved in water by Fenton process wherein the copper-catalyzed hydrogen peroxide (H2O2) reaction makes the resin hydrophilic by the disintegration of polymer matrix. Sonication of the dissolved resin thus obtained made the waste stream more amenable to WAO. Parameters for Fenton dissolution and sonication were studied to aid effective mineralization by WAO. The kinetic studies of WAO were performed using copper sulfate (CuSO4) as the homogeneous catalyst, in the temperature range of 483,523 K. It is thus possible to address the disposal of solid ion exchange resin by the hybrid process, described here. Copyright © 2008 Curtin University of Technology and John Wiley & Sons, Ltd. [source]

Auslegung und Optimierung von hybriden Trennverfahren,

Potential of different techniques of preferential crystallization for enantioseparation of racemic compound forming systems

CHIRALITY, Issue 8 2009
Daniel Polenske
Abstract Recently the feasibility of preferential crystallization for enantioseparation of racemic compound forming systems has been demonstrated (Lorenz et al., Application of preferential crystallization to resolve racemic compounds in a hybrid process. Chirality 2006;18:828,840; Polenske et al., Separation of the propranolol hydrochloride enantiomers by preferential crystallization: thermodynamic basis and experimental verification. Cryst Growth Des 2007;7:1628,1634). Here, the development and the potential of an efficient separation process operated via two different techniques of preferential crystallization are studied: (1) seeded isothermal preferential crystallization and (2) auto-seeded polythermal preferential crystallization. Both techniques were investigated in the batch and in the cyclic operation mode. On the example of mandelic acid as a typical racemic compound forming system, it is demonstrated that a cyclic auto-seeded polythermal process is feasible and significantly more efficient than the seeded isothermal one. Chirality, 2009. © 2008 Wiley-Liss, Inc. [source]

Hydrophobic pervaporation for environmental applications: Process optimization and integration

Geothermal-based hydrogen production using thermochemical and hybrid cycles: A review and analysis

INTERNATIONAL JOURNAL OF ENERGY RESEARCH, Issue 9 2010
M. Tolga Balta
Abstract Geothermal-based hydrogen production, which basically uses geothermal energy for hydrogen production, appears to be an environmentally conscious and sustainable option for the countries with abundant geothermal energy resources. In this study, four potential methods are identified and proposed for geothermal-based hydrogen production, namely: (i) direct production of hydrogen from the geothermal steam, (ii) through conventional water electrolysis using the electricity generated through geothermal power plant, (iii) by using both geothermal heat and electricity for high temperature steam electrolysis and/or hybrid processes, and (iv) by using the heat available from geothermal resource in thermochemical processes. Nowadays, most researches are focused on high-temperature electrolysis and thermochemical processes. Here we essentially discuss some potential low-temperature thermochemical and hybrid cycles for geothermal-based hydrogen production, due to their wider practicality, and examine them as a sustainable option for hydrogen production using geothermal heat. We also assess their thermodynamic performance through energy and exergy efficiencies. The results show that these cycles have good potential and attractive overall system efficiencies over 50% based on a complete reaction approach. The copper-chlorine cycle is identified as a highly promising cycle for geothermal-hydrogen production. Copyright © 2009 John Wiley & Sons, Ltd. [source]

A New Numerical Approach for a Detailed Multicomponent Gas Separation Membrane Model and AspenPlus Simulation

CHEMICAL ENGINEERING & TECHNOLOGY (CET), Issue 7 2005
M. H. Murad Chowdhury
Abstract A new numerical solution approach for a widely accepted model developed earlier by Pan [1] for multicomponent gas separation by high-flux asymmetric membranes is presented. The advantage of the new technique is that it can easily be incorporated into commercial process simulators such as AspenPlusTM [2] as a user-model for an overall membrane process study and for the design and simulation of hybrid processes (i.e., membrane plus chemical absorption or membrane plus physical absorption). The proposed technique does not require initial estimates of the pressure, flow and concentration profiles inside the fiber as does in Pan's original approach, thus allowing faster execution of the model equations. The numerical solution was formulated as an initial value problem (IVP). Either Adams-Moulton's or Gear's backward differentiation formulas (BDF) method was used for solving the non-linear differential equations, and a modified Powell hybrid algorithm with a finite-difference approximation of the Jacobian was used to solve the non-linear algebraic equations. The model predictions were validated with experimental data reported in the literature for different types of membrane gas separation systems with or without purge streams. The robustness of the new numerical technique was also tested by simulating the stiff type of problems such as air dehydration. This demonstrates the potential of the new solution technique to handle different membrane systems conveniently. As an illustration, a multi-stage membrane plant with recycle and purge streams has been designed and simulated for CO2 capture from a 500,MW power plant flue gas as a first step to build hybrid processes and also to make an economic comparison among different existing separation technologies available for CO2 separation from flue gas. [source]